Study on the effect of the porous media equivalent particulate fouling model on heat transfer performance in heat exchanger channels

被引:0
作者
Li, Jiang [1 ]
Han, Zhimin [1 ]
Liu, Wei [1 ]
Wang, Taozhi [1 ]
Chang, Hongliang [1 ]
机构
[1] Northeast Elect Power Univ, Sch Energy & Power Engn, Jilin, Jilin, Peoples R China
关键词
Porous media; Particulate fouling; Heat exchanger; Heat transfer performance; Numerical simulation; PARTICLE DEPOSITION; VORTEX GENERATORS; FLOW; TURBULENT; RESISTANCE; SIMULATION; TRANSPORT; SURFACE;
D O I
10.1016/j.applthermaleng.2025.125709
中图分类号
O414.1 [热力学];
学科分类号
摘要
With the development of modern industry, the issue of particulate fouling deposition within heat exchanger channels has become increasingly severe, significantly reducing heat transfer coefficient and potentially leading to hazards such as tube rupture and low efficiency. To investigate the impact of particulate fouling on heat transfer performance in heat exchanger channels, this paper proposes a porous media equivalent particulate fouling model, which has been experimentally validated for accuracy. The model is applied to both smooth and complex heat exchanger channels, with a comparative analysis focusing on the changes in fouling resistance and Nusselt number between the porous media equivalent particulate fouling model and the traditional particulate fouling model. Additionally, the study provides a detailed examination of the effect of fouling layer thickness on heat transfer performance in complex channels. The results indicate that the simulation results using the porous media equivalent particulate fouling model show a higher correlation with experimental data, with the average error reduced by 5.48 %. In both smooth and complex heat exchanger channels, fouling resistance increases progressively along the channel, while the Nusselt number decreases. In the complex channel, due to the influence of vortex generators, fouling resistance and Nusselt number exhibit periodic variations. When the porous media equivalent particulate fouling model is used, the obstruction effect of the fouling layer on the flow field is considered, resulting in a significant increase in fouling resistance, which in turn reduces the Nusselt number. Furthermore, in the complex channel, as particle concentration increases, the fouling layer thickness gradually increases. When the fouling layer reaches a thickness of 0.42 mm, the heat transfer efficiency decreases by 12.1 %, while flow resistance increases by 36.0 %.
引用
收藏
页数:11
相关论文
共 44 条
  • [1] Li J., Yang J., Liu M., Ma Z., Fang W., Bi J., Quality matters: pollution exacerbates water scarcity and sectoral output risks in China, Water Res., 224, (2022)
  • [2] Wang J., Liang Y., Anti-fouling effect of axial alternating electromagnetic field on calcium carbonate fouling in U-shaped circulating cooling water heat exchange tube, Int. J. Heat. Mass. Tran., 115, pp. 774-781, (2017)
  • [3] Kong D., Chen W., Niu X., Liu C., Isaev S.A., Guo T., A comparative study of internal heat transfer enhancement of impingement/effusion cooling roughened by solid rib and slit rib, Phy, Fluids., 36, 1, (2024)
  • [4] Epstein N., Fouling in heat exchangers, (1978)
  • [5] Wang F.L., He Y.L., Tong Z.X., Tang S.Z., Real-time fouling characteristics of a typical heat exchanger used in the waste heat recovery systems, Int. J. Heat. Mass. Transf., 104, pp. 775-786, (2017)
  • [6] Han H., He Y.L., Tao W.Q., Li Y.S., A parameter study of tube bundle heat exchangers for fouling rate reduction, Int. J. Heat. Mass. Transf., 72, pp. 210-221, (2014)
  • [7] Han Z.M., Xu Z.M., Sun A.D., Yu X.Y., The deposition characteristics of micron particles in heat exchange pipelines, Appl. Therm. Eng., 158, (2019)
  • [8] Guha A., A unified Eulerian theory of turbulent deposition to smooth and rough surfaces, J. Aerosol Sci., 28, 8, pp. 1517-1537, (1997)
  • [9] Paz C., Suarez E., Eiris A., Porteiro J., Development of a predictive CFD fouling model for diesel engine exhaust gas systems, Heat. Transf. Eng., 34, 8-9, pp. 674-682, (2013)
  • [10] Guha A., Transport and deposition of particles in turbulent and laminar flow, Annu. Rev. Fluid. Mech., 40, pp. 311-341, (2008)